• Journal of the Korean Society of Marine Environment & Safety
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• v.23 no.5
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• pp.541-548
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• 2017

A theoretical study on gas-liquid two-phase flow flushing systemnitrogen gas to the oil used for existing flushing equipment was conducted on the basis of ISO code so as to improve performance of existing high-temperature oil flushing equipment used in ocean plant facility drying field. For study, we analyzed process simulation results mixed fluid mixing ratio, temperature, Reynolds number and liquid hold up affectcleaning performance after designing oil-nitrogen gas mixture flushing system process. As a result, as the volume flow rate of mixed fluid increases with the tube diameter the volume fraction of the gas phase constant, the liquid fraction difference value at the inlet and outlet of horizontal hydraulic piping increases. It was found that the phase distribution between oil and nitrogen gas bubbles varies depending on the position the pipe lengthdirection. This change in phase distribution is expected to have a significant impact on the clean performance of an oil-nitrogen gas mixture flushing system.

• Proceedings of the Korean Nuclear Society Conference
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• 1995.05a
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• pp.531-537
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• 1995

본 논문에서는 증기폭발의 전파과정을 해석하기 위한 수학적 모델을 제시하였다. 이 모델은 용융물, 용융파편, 그리고 냉각재 기상과 액상 둥 4상 유체의 2차원적인 천이거동을 지배방정식 및 관련상관식의 수치적 해를 구함으로써 증기폭발의 전파속도 및 폭발압력 등을 예측할 수 있다. 모델에 사용된 주요 상관식은 용융물 분쇄, 냉각재 상변화, 에너지 교환, 그리고 운동량 교환함으로 구성되어 있다. 냉각재의 상태를 결정하는데 있어서 냉각재의 기상과 액상 사이의 열역학적인 비평형을 허용할 수 있도록 냉각재의 상태방정식을 구성하였다. 주석/물의 증기폭발에 대한 예제계산을 수행한 결과 폭발의 전파속도 및 압력 등에 있어서 합당한 것으로 밝혀졌다. 또한 중요한 초기변수(중기 분율, 용융물 분율) 및 관련상관식에 대한 민감도 분석을 수행함으로써 모델개선을 위한 중요인자를 제시하였다.

• Applied Chemistry for Engineering
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• v.16 no.6
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• pp.848-852
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• 2005

The two important problems to solve before the industrialization of the iodine-sulfur (IS) process are (i) methods to separate $H_2SO_4$ and HI and (ii) to maintain constant components. However undesired reaction was occurred and $H_2S$ and S were formed during the Bunsen reaction. It is necessary to forbid the undesired reaction between $H_2SO_4$ and HI by separating the two acids into two different layers. The experimental conditions for the present study was chosen in such a way that to achieve the separation between the two acids and minimize the side reaction. $H_2S$ formation was reduced and the separations of the two liquids were occurred at $H_2O$ molar fraction from 0.86 to 0.909. But the separations between the two liquids were not occurred at $H_2O$ molar fraction more than 0.92.

• Korean Chemical Engineering Research
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• v.49 no.1
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• pp.83-88
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• 2011

Holdup characteristics of small bubbles were investigated in a viscous slurry bubble column. The phase holdup of small bubbles was obtained from the knowledge of total bubble(gas) holdup and large bubble holdup, which were measured by mean of static pressure drop method and dual resistivity probe method, respectively. Effects of gas velocity, viscosity of continuous liquid phase and solid fraction in the slurry phase on the small bubble holdup as well as holdups of total bubble(gas) and large bubble in a viscous slurry bubble column. The small bubble holdup increased with increasing gas velocity but decreased with increasing liquid viscosity or solid fraction in the slurry phase. In addition the fraction of small bubble in the total bubble(gas) holdup increased with increasing gas velocity but decreased with increasing liquid viscosity or solid fraction in the slurry phase. It was revealed that the rising velocity of large bubble did not related to the holdup of small bubble in a viscous slurry bubble column.

• Clean Technology
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• v.12 no.1
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• pp.45-51
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• 2006

Colloidal Liquid Aphrons(CLAs) were prepared from different solvents such as nonpolar hydrocarbons, alcohols, and amines. Water-soluble surfactant and oil-soluble surfactant were used in this study. The effect of PVR (phase volume ratio) and concentration of extractant on the stability of CLA was investigated. The stability of CLA was affected by PVR. As PVR was increased, the stability of CLA was decreased.

• Korean Chemical Engineering Research
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• v.50 no.3
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• pp.499-504
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• 2012

Characteristics of overall heat transfer were investigated in a three-phase slurry bubble column with relatively low surface tension media, which has been frequently encountered in the fields of industry. The heat transfer phenomena was examined in the system which was composed of a coaxial vertical heater and a proper of bubble column. The heat transfer coefficient was estimated from the measured mean value of temperature difference between the heater surface and the column proper at the steady state condition. Effects of gas velocity ($U_G$), solid fraction in the slurry phase ($C_S$) and surface tension (${\sigma}_L$) of continuous liquid media on the overall heat transfer coefficient (h) in the bubble column were determined. The mean value of temperature difference was estimated from the data of temperature difference fluctuations with a variation of time. The amplitude and mean value of temperature difference fluctuations with respect to the elasped time appeared to decrease with decreasing the surface tension of liquid phase. The overall heat transfer coefficient between the immersed heated and the bubble column increased with an increase in the gas velocity or solid fraction in the slurry phase, but it decreased with an increase in the surface tension of continuous liquid media. The overall heat coefficient in the slurry bubble column with relatively low surface tension media was well correlated in term of operating variables and dimensionless groups within this experimental conditions.

• The Korean Journal of Rheology
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• v.10 no.1
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• pp.24-30
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• 1998

솔젤법을 이용하여 단분산의 실리카 입자를 제조하고 농도변화에 따른 실리카 분산 액의 유변학적 거동을 해석하였다. 단분산 실리카 입자의 제조는 솔젤법을 이용한 액상반으 으로 제조하였고 입자의 안정화를 위하여 입자표면에 실란커플링제를 코팅하여 유기용매에 서 안정성을 갖도록 하였다. 분산액의 농도에 따른 유변학적 거동을 조사하기 위하여 부피 분율( )이 0.05인 희박 분산계로부터 =0.55의 고농도 분산계를 제조하였다. 솔젤법을 통하 여 단분산 실리카 입자를 성공적으로 제조하였으며 실란커플링제인 ${\gamma}$-methacryloxypropyl triethoxysilane로 입자의 표면을 화학적 방법으로 처리하여 유기용매 상에서 알킬기의 작용 에 의한 hard-sphere'특성을 나타내도록 하였으며 동시에 분산안정성을 유지할수 있었다. 입자 분산계는 =0.25이하의 부피농도에서는 분산용매와 같은 뉴톤거동을 보여주었으며 이 이이상의 농도에서는 비뉴톤거동인 전단담화(shear thinning)현상과 high shear limiting viscosity를 나타내었다. 이결과는 Krieger-Dougherty 식을 따름이 확인되었으며 부피분율 =0.50정도까지도 이식이 잘적용됨을 확인하였다. 부피분율 =0.50 이상의 고농도 입자 분산계 는 급격한 점도의 증가와 함께 전단담화와 전단탁화(shear thickening)현상이 모두 관찰되었 다. 특히 전단탁화를 일으키는 특헝전단변형률(cr)이하의 전단변형률에서는 안정되고 빠른 점성반응(viscous response)을 보여주었으나 특성 전단변형률 부근과 이상의 전단변형률 영 역에서는 매우 불안한 거동이 보여짐을 확인하였다. 그러나 이러한 점도 거동은 가역적이며 전단변형률을 증가시킬때와 감소시킬 때의 유변학적 거동이 거의 일치하였다.

• Journal of computational fluids engineering
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• v.8 no.3
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• pp.12-20
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• 2003

A numerical procedure for the calculation of solidification and melting phase change using PISO algorithm is presented. In case of phase change problem, the coupling between velocity/pressure/temperature and liquid fraction is important. The converged temperature and liquid fraction solution which satisfies the energy balance is acquired by applying enthalpy method into inner iteration in matrix solver. And a modified PISO algorithm version is introduced to properly solve the coupling between velocity/pressure/temperature and liquid fraction. A comparison of the proposed procedure with a standard iterative method shows improvement both in terms of computing speed and robustness.

• Korean Journal of Air-Conditioning and Refrigeration Engineering
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• v.9 no.4
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• pp.527-535
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• 1997

Vapor-liquid equilibrium apparatus is designed and set up. The vapor-liquid equilibrium data of the binary system HFC32/134a are measured in the range between 258.15 and 283.15K at compositions of 0.2, 0.4, 0.6 and 0.8 mole fraction of HFC32. Twenty-two equilibrium data are obtained. Based upon the present data, the binary interaction parameter for Carnahan-Starling-De Santis equation of state is calculated. Temperature range of data is extended to 313.04K using the data in the open literatures. Interaction parameters are determined at nine isotherms.

• Korean Chemical Engineering Research
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• v.49 no.2
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• pp.200-205
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• 2011

Axial and radial distributions of bubble holdup were investigated in a slurry bubble column with pilot plant scale(D=1.0 m). Effects of gas velocity, surface tension of continuous liquid medium and solid fraction in the slurry phase on the axial and radial distributions of bubble holdup were examined. The bubble holdup decreased with increasing radial dimensionless distance from the center of the column, while it increased with increasing dimensionless distance in the axial direction from the distributor, in all the cases studied. The radial non-uniformity of bubble holdup increased with increasing gas velocity but decreasing surface tension of liquid medium, while it was not dependent upon the solid fraction in the slurry phase. The axial non-uniformity of bubble holdup increased with increasing gas velocity, but it does not change considerably with variations of liquid surface tension or solid fraction in the slurry phase . The axial and radial distributions of bubble holdup were well correlated in terms of operating variables within this experimental conditions.